Hydraulic Engineering: cram pack

Formula sheets, the key method steps for every topic and 10 practice problems, with full solutions at the back.

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1Formulas and methods

Hydrostatic force

Pressure at depth
p = ρgh
Force on a vertical wall
F = ρg·hc·A
Centre of pressure
yp = yc + Ic/(ycA)
Rectangle
Ic = bH³/12

Continuity & Bernoulli

Continuity
A1v1 = A2v2
Bernoulli
p1 + ½ρv1² + ρgz1 = p2 + ½ρv2² + ρgz2
Flow rate
Q = A·v
Circle area
A = πd²/4

Pipe friction & head loss

Reynolds number
Re = V·D/ν = ρ·V·D/μ
Flow regime
laminar below Re ≈ 2000, turbulent above Re ≈ 4000
Mean velocity
V = Q/A, A = π·D²/4
Darcy–Weisbach
hf = f·(L/D)·V²/(2g)
Minor losses
hm = ΣK·V²/(2g)
Typical K values
entrance 0.5, exit 1.0, 90° bend ≈ 0.3
Pressure drop
Δp = ρ·g·hf
Two open reservoirs
Δz = (f·L/D + ΣK)·V²/(2g)
Free outlet
H = (1 + f·L/D + ΣK)·V²/(2g)

Pumps & pump power

Hydraulic power
Ph = ρ·g·Q·H = Q·Δp
Shaft power
Pshaft = Ph/ηpump
Electrical power
Pel = Pshaft/ηmotor
Pump head
H = Δz + Δp/(ρ·g) + hL
System losses
hL = (f·L/D + ΣK)·V²/(2g)

Open-channel flow (Manning)

Manning equation
V = (1/n)·R2/3·S1/2
Flow rate
Q = A·V
Hydraulic radius
R = A/P (P = wetted perimeter, free surface excluded)
Rectangle
A = b·y, P = b + 2y
Trapezoid (side slope z:1)
A = (b + z·y)·y, P = b + 2y·√(1 + z²)
Circular pipe, full or half full
R = D/4
Required slope
S = (n·Q/(A·R2/3))²

2Practice problems

1.Hydrostatic forceMedium
gated = 4 mH = 2 m

A vertical rectangular gate 2 m wide sits in the wall of a tank of water, with its top edge 4 m below the surface. Find the resultant hydrostatic force F on the gate.

d = 4 mH = 2 mb = 2 mρ = 1000 kg/m³g = 9.81 m/s²
F = kN
2.Hydrostatic forceHard
gated = 1 mH = 2.5 m

A vertical rectangular gate 1.5 m wide sits in the wall of a tank of oil, with its top edge 1 m below the surface. Find the resultant hydrostatic force F on the gate.

d = 1 mH = 2.5 mb = 1.5 mρ = 880 kg/m³g = 9.81 m/s²
F = kN
3.Continuity & BernoulliMedium
Q = ?d = 25 mm, Cd​ = 0.62h = 2.5 m

Water drains from a large open tank through a sharp-edged orifice with a diameter of 25 mm. The water level is kept 2.5 m above the orifice and the discharge coefficient is 0.62. Find the flow rate Q. Use g = 9.81 m/s².

d = 25 mmh = 2.5 mCd = 0.62g = 9.81 m/s²
Q = L/s
4.Continuity & BernoulliHard
pair​ = 40 kPav = ?d = 40 mmh = 1.5 m

A closed water tank has compressed air above the water at a gauge pressure of 40 kPa. Water leaves through an opening with a diameter of 40 mm, 1.5 m below the water surface, into the open air. Ignoring losses, find the jet velocity v. Use g = 9.81 m/s².

pair = 40 kPa (gauge)h = 1.5 md = 40 mmρ = 1000 kg/m³g = 9.81 m/s²
v = m/s
5.Pipe friction & head lossMedium
Q = 80 L/sD = 250 mmL = 500 mf = 0.02

Water flows at 80 L/s through a pipe 500 m long with an inside diameter of 250 mm. Use the Darcy friction factor f = 0.02 and g = 9.81 m/s². Find the friction head loss hf.

Q = 80 L/sL = 500 mD = 250 mmf = 0.02g = 9.81 m/s²
hf = m
6.Pipe friction & head lossHard
K = 2free outletH = ?L = 200 m, D = 150 mm, f = 0.0152× bend (K = 0.3)

A pipe 200 m long with an inside diameter of 150 mm (Darcy friction factor f = 0.015) runs from an open reservoir and discharges as a free jet into the air. The minor losses are a square-edged entrance (K = 0.5), 2 bends (K = 0.3 each) and a valve (K = 2). Use g = 9.81 m/s². How far H must the reservoir surface be above the pipe outlet for a flow rate of 40 L/s?

Q = 40 L/sL = 200 mD = 150 mmf = 0.015Kentrance = 0.5Kbend = 0.3 (×2)Kvalve = 2
H = m
7.Pumps & pump powerMedium
PQ = 50 L/sH = 56 m

A pump delivers 50 L/s of water (ρ = 1000 kg/m³) against a head of 56 m. The pump efficiency is 60% and the electric motor driving it has an efficiency of 94%. Use g = 9.81 m/s². Find the electrical power Pel the motor draws, in kW.

Q = 50 L/sH = 56 mηpump = 60%ηmotor = 94%g = 9.81 m/s²
Pel = kW
8.Pumps & pump powerHard
PQ = 75 L/sΔz = 5 mL = 100 m, D = 200 mm, f = 0.025, ΣK = 2.5

A pump moves 75 L/s of water (ρ = 1000 kg/m³) from an open lower reservoir to an upper tank whose water surface is 5 m higher. The pipe is 100 m long with an inside diameter of 200 mm and a Darcy friction factor f = 0.025; the minor-loss coefficients add up to ΣK = 2.5 (entrance and exit included). Use g = 9.81 m/s². The pump efficiency is 70%. Find the shaft power Pshaft in kW.

Q = 75 L/sΔz = 5 mL = 100 mD = 200 mmf = 0.025ΣK = 2.5η = 70%
Pshaft = kW
9.Open-channel flow (Manning)Medium
D = 900 mmn = 0.013, S = 0.005

A concrete storm sewer with an inside diameter of 900 mm flows half full. Manning n = 0.013 and the slope is S = 0.005. Find the flow rate Q in m³/s.

D = 900 mmn = 0.013S = 0.005
Q = m³/s
10.Open-channel flow (Manning)Hard
b = 2 my = 1.7 m1 : 1n = 0.025, Q = 17 m³/s

A trapezoidal gravel channel with a bottom width of 2 m and side slopes of 1:1 (horizontal:vertical) must carry 17 m³/s in uniform flow at a depth of 1.7 m. Manning n = 0.025. Find the required bed slope S (in m/m).

Q = 17 m³/sb = 2 my = 1.7 mz = 1n = 0.025
S = m/m

3Solutions

1.Hydrostatic force

Answer: F = 196.2 kN

Hydrostatic force on a plane surface: F = ρ·g·yc·A. It acts at the centre of pressure, ycp = yc + Ic/(ycA), which always lies below the centroid.

Centroid depth and area

yc = d + H/2 = 4 + 2/2 = 5 m
A = H·b = 2·2 = 4 m²
gated = 4 mH = 2 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·5·4 = 196.2 kN

Answer

F = 196.2 kN
2.Hydrostatic force

Answer: F = 72.84 kN

Hydrostatic force on a plane surface: F = ρ·g·yc·A. It acts at the centre of pressure, ycp = yc + Ic/(ycA), which always lies below the centroid.

Centroid depth and area

yc = d + H/2 = 1 + 2.5/2 = 2.25 m
A = H·b = 2.5·1.5 = 3.75 m²
gated = 1 mH = 2.5 mF

Resultant force

F = ρ·g·yc·A = 880·9.81·2.25·3.75 = 72.84 kN

Answer

F = 72.84 kN
3.Continuity & Bernoulli

Answer: Q = 2.131 L/s

Continuity and Bernoulli: for an incompressible fluid the flow rate is the same at every section, Q = A₁v₁ = A₂v₂. Along a streamline without losses, p + ½ρv² + ρgz is constant, so where the fluid is faster or higher its pressure is lower.

Ideal jet velocity

√(2gh) = √(2·9.81·2.5) = 7.004 m/s

Actual flow rate

The discharge coefficient accounts for the contraction of the jet and friction at the edge.

Q = Cd·A·√(2gh) = 0.62·0.0004909·7.004 = 0.002131 m³/s = 2.131 L/s

Answer

Q = 2.131 L/s
4.Continuity & Bernoulli

Answer: v = 10.46 m/s

Continuity and Bernoulli: for an incompressible fluid the flow rate is the same at every section, Q = A₁v₁ = A₂v₂. Along a streamline without losses, p + ½ρv² + ρgz is constant, so where the fluid is faster or higher its pressure is lower.

Bernoulli from the surface to the jet

v = √(2·(40000/1000 + 9.81·1.5)) = 10.46 m/s

Answer

v = 10.46 m/s
5.Pipe friction & head loss

Answer: hf = 5.415 m

Pipe flow: the Reynolds number Re = V·D/ν = ρ·V·D/μ tells laminar flow (Re below about 2000) from turbulent flow (above about 4000). Friction along a pipe costs the Darcy–Weisbach head loss hf = f·(L/D)·V²/(2g). Fittings, valves, the entrance and the exit add minor losses hm = ΣK·V²/(2g). Between two open reservoir surfaces the energy equation gives Δz = hf + hm, with the exit loss K = 1 included.

Mean velocity

A = π·0.25²/4 = 0.04909 m²
V = Q/A = 0.08/0.04909 = 1.63 m/s

Velocity head

V²/(2g) = 1.63²/(2·9.81) = 0.1354 m

Darcy–Weisbach

hf = f·(L/D)·V²/(2g) = 0.02·(500/0.25)·1.63²/(2·9.81) = 5.415 m

Answer

hf = 5.415 m
6.Pipe friction & head loss

Answer: H = 6.294 m

Pipe flow: the Reynolds number Re = V·D/ν = ρ·V·D/μ tells laminar flow (Re below about 2000) from turbulent flow (above about 4000). Friction along a pipe costs the Darcy–Weisbach head loss hf = f·(L/D)·V²/(2g). Fittings, valves, the entrance and the exit add minor losses hm = ΣK·V²/(2g). Between two open reservoir surfaces the energy equation gives Δz = hf + hm, with the exit loss K = 1 included.

Velocity

V = Q/A = 0.04/0.01767 = 2.264 m/s
V²/(2g) = 0.2611 m

Loss coefficients

f·L/D = 0.015·200/0.15 = 20
ΣK = 0.5 + 2·0.3 + 2 = 3.1

Energy equation

The outlet jet still carries its velocity head; it is not a loss but it has to be supplied.

H = (1 + 20 + 3.1)·0.2611 = 6.294 m

Answer

H = 6.294 m
7.Pumps & pump power

Answer: Pel = 48.7 kW

Pump power: the power given to the water is the hydraulic power Ph = ρ·g·Q·H = Q·Δp. The shaft must deliver more because the pump loses some: Pshaft = Ph/ηpump, and the motor draws Pel = Pshaft/ηmotor. The pump head H follows from the energy equation: static lift + pressure head + all friction and minor losses.

Hydraulic power

Ph = ρ·g·Q·H = 1000·9.81·0.05·56 = 27.47 kW

Shaft power

Pshaft = 27.47/0.6 = 45.78 kW

Electrical power

Pel = 45.78/0.94 = 48.7 kW

Answer

Pel = 48.7 kW
8.Pumps & pump power

Answer: Pshaft = 9.835 kW

Pump power: the power given to the water is the hydraulic power Ph = ρ·g·Q·H = Q·Δp. The shaft must deliver more because the pump loses some: Pshaft = Ph/ηpump, and the motor draws Pel = Pshaft/ηmotor. The pump head H follows from the energy equation: static lift + pressure head + all friction and minor losses.

Velocity

V = Q/A = 0.075/0.03142 = 2.387 m/s
V²/(2g) = 0.2905 m

Head losses

hL = (f·L/D + ΣK)·V²/(2g) = (12.5 + 2.5)·0.2905 = 4.357 m

Pump head

H = Δz + hL = 5 + 4.357 = 9.357 m

Shaft power

Pshaft = ρ·g·Q·H/η = 1000·9.81·0.075·9.357/0.7 = 9.835 kW

Answer

Pshaft = 9.835 kW
9.Open-channel flow (Manning)

Answer: Q = 0.64 m³/s

Manning’s equation (SI): for uniform flow in an open channel V = (1/n)·R2/3·S1/2 and Q = A·V, with n the roughness coefficient, S the bed slope (m/m) and R = A/P the hydraulic radius: flow area divided by wetted perimeter. Only the boundary in contact with the water counts in P, not the free surface. Rectangle: A = b·y, P = b + 2y. Trapezoid with side slopes z:1 (horizontal:vertical): A = (b + z·y)·y, P = b + 2y·√(1 + z²). A circular pipe flowing full or half full has R = D/4.

Geometry

A = 0.3181 m², R = D/4 = 0.225 m

Velocity

V = (1/0.013)·0.2252/3·0.0051/2 = 2.012 m/s

Flow rate

Q = A·V = 0.3181·2.012 = 0.64 m³/s

Answer

Q = 0.64 m³/s
10.Open-channel flow (Manning)

Answer: S = 0.005074 m/m

Manning’s equation (SI): for uniform flow in an open channel V = (1/n)·R2/3·S1/2 and Q = A·V, with n the roughness coefficient, S the bed slope (m/m) and R = A/P the hydraulic radius: flow area divided by wetted perimeter. Only the boundary in contact with the water counts in P, not the free surface. Rectangle: A = b·y, P = b + 2y. Trapezoid with side slopes z:1 (horizontal:vertical): A = (b + z·y)·y, P = b + 2y·√(1 + z²). A circular pipe flowing full or half full has R = D/4.

Geometry

A = (b + z·y)·y = (2 + 1·1.7)·1.7 = 6.29 m²
P = b + 2y·√(1 + z²) = 2 + 2·1.7·√(1 + 1²) = 6.808 m
R = A/P = 0.9239 m

Solve Manning for S

S1/2 = n·Q/(A·R2/3) = 0.025·17/(6.29·0.9486) = 0.07123
S = 0.07123² = 0.005074

Answer

S = 0.005074

That is a fall of 5.074 m per kilometre.

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